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Journal ArticleDOI

Independent prediction of slip velocity and hold-up in liquid/liquid extraction columns

TLDR
The correlation of slip velocity using a large bank of published data for pulsed perforated plate, Karr reciprocating-plate, rotating disc and spray extraction columns is presented in this article.
Abstract
The correlation of slip velocity using a large bank of published data for pulsed perforated-plate, Karr reciprocating-plate, rotating disc and spray extraction columns is presented. Based on more than 3,700 data points with and without mass transfer, empirical equations not including hold-up for each of the columns are suggested which reproduce the slip velocity data over a wide range of variables. Explicit correlations for hold-up in both the loose and dense-packed regions of operation in spray columns are also presented which do not involve slip velocity. The equations presented are more exact and simpler to use than previous empirical correlations; these often involve the characteristic velocity which is difficult to accurately predict.

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Citations
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Journal ArticleDOI

Modeling of liquid-liquid extraction column: a review

TL;DR: In this article, a review of various types of commonly used extraction columns, viz. pulsed sieve plate column, rotating disc contactor, Kuhni column, spray column, Scheibel extractor, packed column, Oldshue-Rushton contactor and reciprocating plate column are presented.
Journal ArticleDOI

Hydrodynamic and mass transfer characteristics of asymmetric rotating disc extractors

TL;DR: In this paper, measurements of dispersed phase hold-up (∈D), effective interfacial area ( a _ ), continuous phase mass transfer coefficient ( k C a ) and axial dispersion coefficient for the dispersed as well as continuous phase have been performed in 80mm and 150mm i.d. ARDC over a wide range of operating variables and physical properties.
Journal ArticleDOI

Dispersed phase holdup in a pulsed disc and doughnut extraction column

TL;DR: In this article, a 76 mm diameter pulsed disc and doughnut extraction column for three different liquid-liquid systems was investigated and the effects of operational variables such as pulsation intensity and dispersed and continuous phase flow rates on holdup was found to be significant.
Journal ArticleDOI

Holdup, characteristic velocity and slip velocity between two phases in a multi-impeller column for high/medium/low interfacial tension systems

TL;DR: In this paper, the effects of the agitation speed, dispersed as well as continuous phase velocity, direction of mass transfer, and interfacial tension were studied for determination of holdup, slip velocity and characteristic velocity in a multi-impeller column.
References
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Journal ArticleDOI

Drag coefficient and relative velocity in bubbly, droplet or particulate flows

TL;DR: In this article, the relative motion correlations for dispersed two-phase flows of bubbles, drops, and particles were developed from simple similarity criteria and a mixture viscosity model, and satisfactory agreements were obtained at wide ranges of the particle concentration and Reynolds number.
Journal ArticleDOI

Drop size and holdup in a reciprocating plate extraction column

TL;DR: In this article, the Sauter mean droplet diameter was found to depend on the product of plate amplitude and frequency and on the system properties, but it was not in general affected by the throughput.
Journal ArticleDOI

Gravity settling in liquid/liquid dispersions

TL;DR: In this paper, an empirical expression for the prediction of dispersed phase hold-up and slip velocity in droplet dispersions settling under gravity is presented, based on 998 published experimental results for 29 liquid/liquid systems from 14 different data sources.
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